Mixture of Hexanedioic acid, dimethyl ester + Butanedioic acid, dimethyl ester

Datasets

1. Mole fraction (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Butanedioic acid, dimethyl ester (2) [ref]

Fixed		Measured
Mole fraction of Butanedioic acid, dimethyl ester (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Butanedioic acid, dimethyl ester (2) - Gas
0.0000	2.00	0.0000
0.0460	2.00	0.1778
0.1508	2.00	0.4434
0.2403	2.00	0.5812
0.3444	2.00	0.6915
0.4160	2.00	0.7527
0.4990	2.00	0.8083
0.5101	2.00	0.8107
0.5746	2.00	0.8463
0.6792	2.00	0.8924
0.7372	2.00	0.9101
0.8251	2.00	0.9410
0.9026	2.00	0.9671
0.9721	2.00	0.9902
1.0000	2.00	1.0000
0.0000	5.20	0.0000
0.0375	5.20	0.1580
0.1222	5.20	0.3954
0.2301	5.20	0.5709
0.3263	5.20	0.6771
0.3763	5.20	0.7236
0.4428	5.20	0.7698
0.4871	5.20	0.7994
0.5928	5.20	0.8591
0.6687	5.20	0.8939
0.7279	5.20	0.9181
0.8126	5.20	0.9478
0.9167	5.20	0.9788
0.9767	5.20	0.9943
1.0000	5.20	1.0000
0.0000	8.30	0.0000
0.0449	8.30	0.1651
0.1597	8.30	0.4451
0.2687	8.30	0.6115
0.3393	8.30	0.6851
0.4115	8.30	0.7414
0.4547	8.30	0.7721
0.4929	8.30	0.7974
0.6217	8.30	0.8648
0.6908	8.30	0.8938
0.7726	8.30	0.9270
0.8749	8.30	0.9627
0.9164	8.30	0.9750
0.9730	8.30	0.9922
1.0000	8.30	1.0000

Mole fraction of Butanedioic acid, dimethyl ester (2) [ref]

Fixed		Measured
Mole fraction of Butanedioic acid, dimethyl ester (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Butanedioic acid, dimethyl ester (2) - Gas
0.0000	2.00	0.0000
0.0460	2.00	0.1778
0.1508	2.00	0.4434
0.2403	2.00	0.5812
0.3444	2.00	0.6915
0.4160	2.00	0.7527
0.4990	2.00	0.8083
0.5101	2.00	0.8107
0.5746	2.00	0.8463
0.6792	2.00	0.8924
0.7372	2.00	0.9101
0.8251	2.00	0.9410
0.9026	2.00	0.9671
0.9721	2.00	0.9902
1.0000	2.00	1.0000
0.0000	5.20	0.0000
0.0375	5.20	0.1580
0.1222	5.20	0.3954
0.2301	5.20	0.5709
0.3263	5.20	0.6771
0.3763	5.20	0.7236
0.4428	5.20	0.7698
0.4871	5.20	0.7994
0.5928	5.20	0.8591
0.6687	5.20	0.8939
0.7279	5.20	0.9181
0.8126	5.20	0.9478
0.9167	5.20	0.9788
0.9767	5.20	0.9943
1.0000	5.20	1.0000
0.0000	8.30	0.0000
0.0449	8.30	0.1651
0.1597	8.30	0.4451
0.2687	8.30	0.6115
0.3393	8.30	0.6851
0.4115	8.30	0.7414
0.4547	8.30	0.7721
0.4929	8.30	0.7974
0.6217	8.30	0.8648
0.6908	8.30	0.8938
0.7726	8.30	0.9270
0.8749	8.30	0.9627
0.9164	8.30	0.9750
0.9730	8.30	0.9922
1.0000	8.30	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butanedioic acid, dimethyl ester (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	2.00	390.98
0.0460	2.00	388.35
0.1508	2.00	383.43
0.2403	2.00	379.83
0.3444	2.00	376.35
0.4160	2.00	374.21
0.4990	2.00	372.46
0.5101	2.00	372.18
0.5746	2.00	370.96
0.6792	2.00	368.81
0.7372	2.00	367.52
0.8251	2.00	365.95
0.9026	2.00	364.30
0.9721	2.00	363.97
1.0000	2.00	363.39
0.0000	5.20	410.82
0.0375	5.20	407.99
0.1222	5.20	402.49
0.2301	5.20	398.13
0.3263	5.20	395.29
0.3763	5.20	393.98
0.4428	5.20	392.60
0.4871	5.20	391.51
0.5928	5.20	389.56
0.6687	5.20	388.01
0.7279	5.20	386.74
0.8126	5.20	385.21
0.9167	5.20	383.71
0.9767	5.20	382.63
1.0000	5.20	382.13
0.0000	8.30	422.47
0.0449	8.30	419.63
0.1597	8.30	412.82
0.2687	8.30	408.30
0.3393	8.30	406.13
0.4115	8.30	404.22
0.4547	8.30	403.17
0.4929	8.30	402.17
0.6217	8.30	399.75
0.6908	8.30	398.62
0.7726	8.30	397.42
0.8749	8.30	395.51
0.9164	8.30	394.96
0.9730	8.30	393.92
1.0000	8.30	393.49

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butanedioic acid, dimethyl ester (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	2.00	390.98
0.0460	2.00	388.35
0.1508	2.00	383.43
0.2403	2.00	379.83
0.3444	2.00	376.35
0.4160	2.00	374.21
0.4990	2.00	372.46
0.5101	2.00	372.18
0.5746	2.00	370.96
0.6792	2.00	368.81
0.7372	2.00	367.52
0.8251	2.00	365.95
0.9026	2.00	364.30
0.9721	2.00	363.97
1.0000	2.00	363.39
0.0000	5.20	410.82
0.0375	5.20	407.99
0.1222	5.20	402.49
0.2301	5.20	398.13
0.3263	5.20	395.29
0.3763	5.20	393.98
0.4428	5.20	392.60
0.4871	5.20	391.51
0.5928	5.20	389.56
0.6687	5.20	388.01
0.7279	5.20	386.74
0.8126	5.20	385.21
0.9167	5.20	383.71
0.9767	5.20	382.63
1.0000	5.20	382.13
0.0000	8.30	422.47
0.0449	8.30	419.63
0.1597	8.30	412.82
0.2687	8.30	408.30
0.3393	8.30	406.13
0.4115	8.30	404.22
0.4547	8.30	403.17
0.4929	8.30	402.17
0.6217	8.30	399.75
0.6908	8.30	398.62
0.7726	8.30	397.42
0.8749	8.30	395.51
0.9164	8.30	394.96
0.9730	8.30	393.92
1.0000	8.30	393.49

Sources

• Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa